CN202478807U - Gas desulfurizer - Google Patents
Gas desulfurizer Download PDFInfo
- Publication number
- CN202478807U CN202478807U CN2012200880436U CN201220088043U CN202478807U CN 202478807 U CN202478807 U CN 202478807U CN 2012200880436 U CN2012200880436 U CN 2012200880436U CN 201220088043 U CN201220088043 U CN 201220088043U CN 202478807 U CN202478807 U CN 202478807U
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- liquid plate
- downspout
- sweetening unit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 claims abstract description 42
- 238000006477 desulfuration reaction Methods 0.000 abstract description 8
- 230000000875 corresponding Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 26
- 230000003009 desulfurizing Effects 0.000 description 11
- 238000000034 method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nODVweCcgaGVpZ2h0PSc4NXB4JyB2aWV3Qm94PScwIDAgODUgODUnPgo8IS0tIEVORCBPRiBIRUFERVIgLS0+CjxyZWN0IHN0eWxlPSdvcGFjaXR5OjEuMDtmaWxsOiNGRkZGRkY7c3Ryb2tlOm5vbmUnIHdpZHRoPSc4NS4wJyBoZWlnaHQ9Jzg1LjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8dGV4dCB4PSczNS4wJyB5PSc1My42JyBjbGFzcz0nYXRvbS0wJyBzdHlsZT0nZm9udC1zaXplOjIzcHg7Zm9udC1zdHlsZTpub3JtYWw7Zm9udC13ZWlnaHQ6bm9ybWFsO2ZpbGwtb3BhY2l0eToxO3N0cm9rZTpub25lO2ZvbnQtZmFtaWx5OnNhbnMtc2VyaWY7dGV4dC1hbmNob3I6c3RhcnQ7ZmlsbDojRkNDNjMzJyA+UzwvdGV4dD4KPHBhdGggZD0nTSAzMi43LDM5LjcgTCAzMi43LDM5LjYgTCAzMi43LDM5LjUgTCAzMi43LDM5LjQgTCAzMi43LDM5LjMgTCAzMi42LDM5LjIgTCAzMi42LDM5LjEgTCAzMi41LDM5LjAgTCAzMi41LDM4LjkgTCAzMi40LDM4LjkgTCAzMi4zLDM4LjggTCAzMi4yLDM4LjcgTCAzMi4yLDM4LjcgTCAzMi4xLDM4LjYgTCAzMi4wLDM4LjYgTCAzMS45LDM4LjYgTCAzMS44LDM4LjUgTCAzMS43LDM4LjUgTCAzMS42LDM4LjUgTCAzMS41LDM4LjUgTCAzMS40LDM4LjUgTCAzMS4zLDM4LjYgTCAzMS4yLDM4LjYgTCAzMS4xLDM4LjYgTCAzMS4wLDM4LjcgTCAzMC45LDM4LjcgTCAzMC45LDM4LjggTCAzMC44LDM4LjggTCAzMC43LDM4LjkgTCAzMC42LDM5LjAgTCAzMC42LDM5LjEgTCAzMC41LDM5LjIgTCAzMC41LDM5LjIgTCAzMC41LDM5LjMgTCAzMC40LDM5LjQgTCAzMC40LDM5LjUgTCAzMC40LDM5LjYgTCAzMC40LDM5LjcgTCAzMC40LDM5LjggTCAzMC40LDM5LjkgTCAzMC41LDQwLjAgTCAzMC41LDQwLjEgTCAzMC41LDQwLjIgTCAzMC42LDQwLjMgTCAzMC42LDQwLjQgTCAzMC43LDQwLjUgTCAzMC44LDQwLjUgTCAzMC45LDQwLjYgTCAzMC45LDQwLjcgTCAzMS4wLDQwLjcgTCAzMS4xLDQwLjcgTCAzMS4yLDQwLjggTCAzMS4zLDQwLjggTCAzMS40LDQwLjggTCAzMS41LDQwLjggTCAzMS42LDQwLjggTCAzMS43LDQwLjggTCAzMS44LDQwLjggTCAzMS45LDQwLjggTCAzMi4wLDQwLjggTCAzMi4xLDQwLjcgTCAzMi4yLDQwLjcgTCAzMi4yLDQwLjYgTCAzMi4zLDQwLjYgTCAzMi40LDQwLjUgTCAzMi41LDQwLjQgTCAzMi41LDQwLjMgTCAzMi42LDQwLjMgTCAzMi42LDQwLjIgTCAzMi43LDQwLjEgTCAzMi43LDQwLjAgTCAzMi43LDM5LjkgTCAzMi43LDM5LjggTCAzMi43LDM5LjcgTCAzMS42LDM5LjcgWicgc3R5bGU9J2ZpbGw6IzAwMDAwMDtmaWxsLXJ1bGU6ZXZlbm9kZDtmaWxsLW9wYWNpdHk6MTtzdHJva2U6IzAwMDAwMDtzdHJva2Utd2lkdGg6MC4wcHg7c3Ryb2tlLWxpbmVjYXA6YnV0dDtzdHJva2UtbGluZWpvaW46bWl0ZXI7c3Ryb2tlLW9wYWNpdHk6MTsnIC8+CjxwYXRoIGQ9J00gMzIuNyw0NC4zIEwgMzIuNyw0NC4yIEwgMzIuNyw0NC4xIEwgMzIuNyw0NC4wIEwgMzIuNyw0My45IEwgMzIuNiw0My44IEwgMzIuNiw0My43IEwgMzIuNSw0My43IEwgMzIuNSw0My42IEwgMzIuNCw0My41IEwgMzIuMyw0My40IEwgMzIuMiw0My40IEwgMzIuMiw0My4zIEwgMzIuMSw0My4zIEwgMzIuMCw0My4yIEwgMzEuOSw0My4yIEwgMzEuOCw0My4yIEwgMzEuNyw0My4yIEwgMzEuNiw0My4yIEwgMzEuNSw0My4yIEwgMzEuNCw0My4yIEwgMzEuMyw0My4yIEwgMzEuMiw0My4yIEwgMzEuMSw0My4zIEwgMzEuMCw0My4zIEwgMzAuOSw0My4zIEwgMzAuOSw0My40IEwgMzAuOCw0My41IEwgMzAuNyw0My41IEwgMzAuNiw0My42IEwgMzAuNiw0My43IEwgMzAuNSw0My44IEwgMzAuNSw0My45IEwgMzAuNSw0NC4wIEwgMzAuNCw0NC4xIEwgMzAuNCw0NC4yIEwgMzAuNCw0NC4zIEwgMzAuNCw0NC40IEwgMzAuNCw0NC41IEwgMzAuNCw0NC42IEwgMzAuNSw0NC43IEwgMzAuNSw0NC44IEwgMzAuNSw0NC44IEwgMzAuNiw0NC45IEwgMzAuNiw0NS4wIEwgMzAuNyw0NS4xIEwgMzAuOCw0NS4yIEwgMzAuOSw0NS4yIEwgMzAuOSw0NS4zIEwgMzEuMCw0NS4zIEwgMzEuMSw0NS40IEwgMzEuMiw0NS40IEwgMzEuMyw0NS40IEwgMzEuNCw0NS41IEwgMzEuNSw0NS41IEwgMzEuNiw0NS41IEwgMzEuNyw0NS41IEwgMzEuOCw0NS41IEwgMzEuOSw0NS40IEwgMzIuMCw0NS40IEwgMzIuMSw0NS40IEwgMzIuMiw0NS4zIEwgMzIuMiw0NS4zIEwgMzIuMyw0NS4yIEwgMzIuNCw0NS4xIEwgMzIuNSw0NS4xIEwgMzIuNSw0NS4wIEwgMzIuNiw0NC45IEwgMzIuNiw0NC44IEwgMzIuNyw0NC43IEwgMzIuNyw0NC42IEwgMzIuNyw0NC41IEwgMzIuNyw0NC40IEwgMzIuNyw0NC4zIEwgMzEuNiw0NC4zIFonIHN0eWxlPSdmaWxsOiMwMDAwMDA7ZmlsbC1ydWxlOmV2ZW5vZGQ7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOiMwMDAwMDA7c3Ryb2tlLXdpZHRoOjAuMHB4O3N0cm9rZS1saW5lY2FwOmJ1dHQ7c3Ryb2tlLWxpbmVqb2luOm1pdGVyO3N0cm9rZS1vcGFjaXR5OjE7JyAvPgo8L3N2Zz4K [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 230000037250 Clearance Effects 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000035512 clearance Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 241000893018 Armeria Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The utility model relates to a gas desulfurizer, which belongs to the field of environment-protection equipment. The gas desulfurizer comprises a pot body (8), wherein a gas outlet (1), a desulfuration liquid inlet pipe (2), liquid reduction pipes (3), liquid holding plates (4), a desulfuration liquid outlet pipe (5) and a gas inlet pipe (6) are arranged on the pot body (8); micropores (7) are arranged on the liquid holding plates (4); the liquid reduction pipes (3) pass through the liquid holding plates (4); the liquid holding plates (4) are horizontally distributed in the pot body (8), and the distance between every two adjacent liquid holding plates is equal; the elevation of the lower end of each liquid reduction pipe is lower than the elevation of the upper end of the corresponding adjacent liquid reduction pipe under the each liquid reduction pipe; and the gas inlet pipe (6) is arranged into an I shape and is provided with a downward port.
Description
Technical field
The utility model belongs to the environmental protection equipment field, relates to a kind of device that is used for gas sweetening.
Background technology
H in the gas
2The removing of S has two kinds of dry method and wet methods substantially: dry desulfurization is applicable to the combustion gas that sulfur content is lower, and day output is less.This method technology is simple, and mature and reliable, cost are low, can reach higher degree of purification.But equipment is heavy when adopting this method, and labour intensity was big when also there was the replacing desulfurizing agent in the batch (-type) dry desulfurization, contaminated environment, and waste desulfurizing agent is difficult to problems such as processing.
And in the wet desulfurizing process, desulfurizing tower is the capital equipment that present sulphur is produced, and the major responsibility of desulfurizing tower is the H in the solution absorption gas phase
2S.At present, the version of sulphur tower is more, is main with the packed tower structure how.
The problem that the filling-material structure desulfurizing tower exists is: 1, desulfuration efficiency is low, inefficiency of production; 2, desulfurizing tower is prone to stop up, and takes the whole bag of tricks to handle and all is difficult to take effect, and only takes to stop tower and unloads the filler cleaning, all can influence production and stop tower at every turn, will certainly increase investment if set up stand-by still; 3, doctor solution pipe, gas phase distributor pipe are prone to stop up, and influence the technology operation.
The utility model content
To the deficiency of prior art, the technical problem that the utility model will solve provides a kind of further raising desulfuration efficiency, avoid stopping up, stable operation, reduction process cost, simple in structure, have certain device of the gas sweetening of regulatory function automatically.
In order to solve the problems of the technologies described above, the technical scheme that the utility model provides is:
A kind of gas sweetening unit comprises tank body (8), and tank body (8) sets out gas port (1), doctor solution feed tube (2), downspout (3), holds liquid plate (4), doctor solution drain pipe (5) and air inlet pipe (6), and said holding is provided with aperture (7) on the liquid plate (4).
Said downspout (3) runs through holds liquid plate (4);
Saidly hold that liquid plate (4) horizontal multilayer in tank body (8) is arranged and adjacent liquid plate (4) distance of holding equates;
The said liquid plate (4) of holding is gone up the evenly more aperture (7) of layout number;
The absolute altitude of said downspout (3) lower end is lower than the upper end absolute altitude of its adjacent downspout in below (4);
Said air inlet pipe (6) adopts " worker " font to arrange that port is downward, can adopt the wide aperture structure, should not stop up.
But but the utility model invention has that operating cost is low, operational stability good, desulfurization effect 24 hour operation anti-clogging, a series of technical advantages such as simple in structure, non-maintaining.
Description of drawings
Fig. 1 is the utility model gas sweetening unit structural representation;
Fig. 2 is the utility model gas sweetening unit A-A cross sectional plane sketch map;
Fig. 3 is the utility model gas sweetening unit B-B cross sectional plane sketch map.
The specific embodiment
Below in conjunction with accompanying drawing the utility model gas sweetening unit is elaborated.
Shown in Fig. 1-3, a kind of gas sweetening unit comprises tank body 8, and tank body 8 sets out gas port 1, doctor solution feed tube 2, downspout 3, holds liquid plate 4, doctor solution drain pipe 5 and air inlet pipe 6.Said downspout 3 runs through holds liquid plate 4; The said liquid plate 4 multilayer horizontal arrangement and adjacent in tank body 8 of holding is held liquid plate 4 distances and is equated; Said holding evenly arranged the more aperture 7 of number on the liquid plate 4; The absolute altitude of said downspout 3 lower ends is lower than the upper end absolute altitude of its adjacent downspout 4 in below; Said air inlet pipe 6 adopts " worker " font to arrange that port is downward, can adopt the wide aperture structure, should not stop up.
The process that the gas sweetening unit that uses the utility model to provide carries out desulfurization is following:
Contain H
2The gas of S is through the hypomere of " worker " font air inlet pipe 6 even gas distributions in entering gas sweetening unit tank body; Utilize buoyant gas to be affixed on minimum liquid plate 4 lower surfaces that support; See through the aperture of holding on the liquid plate 47 and evenly mix with the doctor solution of holding between the liquid plate 4, and the H in the gas
2S rapidly with the doctor solution H in the reduction gas that reacts
2The content of S is according to H in the gas
2S content is set the number of plies hold the liquid plate, and reacts through the doctor solution of holding liquid plate 4 and holding between the liquid plate of multilayer, makes H
2The clearance of S reaches requirement, and gas up to standard is collected through gas outlet 1.
Doctor solution gets in the towers through doctor solution feed tube 3, at first holds the liquid plate in the superiors and evenly distributes and utilize gravity to see through to hold 7 of apertures on the liquid plate 4 to advance down one deck and hold liquid plate 4, the H in this process doctor solution and come-up gas
2S reacts rapidly, reduces H in the gas
2The content of S, the doctor solution behind the end reaction is got rid of tank body through doctor solution drain pipe 5.
When equipment normally moved, downspout 3 lower ends were in floodage, and downspout 3 upper ends are in the non-submersion state; The absolute altitude of downspout 3 lower ends is lower than the upper end absolute altitude of its adjacent downspout 4 in below; Like this can be so that surpass when holding liquid plate 4 infiltration capacities when the doctor solution that adds; When holding liquid level on the liquid plate and being higher than the absolute altitude of downspout 3 epimeres; Unnecessary doctor solution also gets into down one decks through downspout 3 and holds liquid plate 4, realizes automatic regulatory function, not only can practice thrift processing cost but also can keep removal effect.
Whole H
2Reaction between S and the doctor solution is adopted reverse-flow, and this makes H
2The clearance of S is higher, the doctor solution utilization rate is higher.
Claims (6)
1. a gas sweetening unit is characterized in that, comprises tank body (8), and tank body (8) sets out gas port (1), doctor solution feed tube (2), downspout (3), holds liquid plate (4), doctor solution drain pipe (5) and air inlet pipe (6), and said holding is provided with aperture (7) on the liquid plate (4).
2. gas sweetening unit according to claim 1 is characterized in that, said downspout (3) runs through holds liquid plate (4).
3. gas sweetening unit according to claim 1 is characterized in that, saidly holds that liquid plate (4) horizontal multilayer in tank body (8) is arranged and adjacent liquid plate (4) distance of holding equates.
4. gas sweetening unit according to claim 1 is characterized in that, the said liquid plate (4) of holding is gone up evenly layout aperture (7).
5. gas sweetening unit according to claim 1 is characterized in that, the absolute altitude of said downspout (3) lower end is lower than the upper end absolute altitude of its adjacent downspout in below (4).
6. gas sweetening unit according to claim 1 is characterized in that, said air inlet pipe (6) adopts " worker " font to arrange that port is downward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200880436U CN202478807U (en) | 2012-03-09 | 2012-03-09 | Gas desulfurizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012200880436U CN202478807U (en) | 2012-03-09 | 2012-03-09 | Gas desulfurizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202478807U true CN202478807U (en) | 2012-10-10 |
Family
ID=46953271
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012200880436U Expired - Fee Related CN202478807U (en) | 2012-03-09 | 2012-03-09 | Gas desulfurizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202478807U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108837688A (en) * | 2018-08-22 | 2018-11-20 | 中国矿业大学 | A kind of flue dust desulfurizer and method |
| CN112023629A (en) * | 2020-08-19 | 2020-12-04 | 盘姜 | Flue gas desulfurization tower and desulfurization method thereof |
-
2012
- 2012-03-09 CN CN2012200880436U patent/CN202478807U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108837688A (en) * | 2018-08-22 | 2018-11-20 | 中国矿业大学 | A kind of flue dust desulfurizer and method |
| CN108837688B (en) * | 2018-08-22 | 2020-07-10 | 中国矿业大学 | Smoke dust desulfurization device and method |
| CN112023629A (en) * | 2020-08-19 | 2020-12-04 | 盘姜 | Flue gas desulfurization tower and desulfurization method thereof |
| CN112023629B (en) * | 2020-08-19 | 2022-05-13 | 上海赛思特新能源科技有限公司 | Flue gas desulfurization tower and desulfurization method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201231130Y (en) | Flue gas desulfurization device for producing ammonia sulfate fertilizer | |
| CN202478807U (en) | Gas desulfurizer | |
| CN203976741U (en) | The organic permeable membrane permeation sepn of high sulfur-containing natural gas desulfurizer | |
| CN205109372U (en) | Remove formaldehyde device | |
| CN206199016U (en) | Gas sweetening hydrogen system | |
| CN204138625U (en) | A kind of offshore platform natural gas desulfurization skid mounted equipment | |
| CN205258394U (en) | Natural gas purifier | |
| CN204051385U (en) | A kind of waste gas purification apparatus | |
| CN204522731U (en) | The outer demist wet flue gas desulfurizer of tower | |
| CN204455038U (en) | Natural-gas desulfurizer | |
| CN202224019U (en) | Flue gas purification equipment | |
| CN202849361U (en) | Hydrogen sulfide treatment device | |
| CN205367975U (en) | Catalyst effluent treatment plant | |
| CN204910875U (en) | A transformer oil water separator for photovoltaic power plant | |
| CN203954995U (en) | Sintering flue gas desulfurization system and desulfurizing agent adding set thereof | |
| CN203700309U (en) | Integrated marsh gas biological desulfuration device | |
| CN203904033U (en) | Oil-separating tank | |
| CN203389515U (en) | Denitration, demercuration and desulfuration combination system device for smoke | |
| CN103601299B (en) | Based on the method for drop biological floating bed raising natural pond liquid N, P, COD clearance | |
| CN202700117U (en) | Flashing dealkylation tank for desulfuration rich liquid | |
| CN202625989U (en) | Integrated buried type scenic water purifying equipment | |
| CN102794086A (en) | Integrated acid-gas sulfur recovery treatment device | |
| CN202621019U (en) | Efficient energy-saving desulfurization and oxidization air pipe | |
| CN202139094U (en) | Electroadsorption waste water desalting device | |
| CN203155076U (en) | Novel desulfurizing tower in series mode |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| C14 | Grant of patent or utility model | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| ASS | Succession or assignment of patent right |
Owner name: SHANDONG LIYUAN HAIDA ENVIRONMENT ENGINEERING CO., Free format text: FORMER OWNER: LIU LEI Effective date: 20130314 |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130314 Address after: 250100 room 702-2, block A, Huaxin Road, Licheng District, Shandong, Ji'nan 15, China Patentee after: Shandong Liyuan Haida Environment Engineering Co., Ltd. Address before: 250100 Shandong city of Ji'nan province high tech Zone Qing Shun Road three century wealth center A3 block 618 Patentee before: Liu Lei |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121010 Termination date: 20170309 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |